JPH04264195A - Production of coke - Google Patents
Production of cokeInfo
- Publication number
- JPH04264195A JPH04264195A JP2455891A JP2455891A JPH04264195A JP H04264195 A JPH04264195 A JP H04264195A JP 2455891 A JP2455891 A JP 2455891A JP 2455891 A JP2455891 A JP 2455891A JP H04264195 A JPH04264195 A JP H04264195A
- Authority
- JP
- Japan
- Prior art keywords
- coke
- less
- sintered ore
- strength
- production
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000000571 coke Substances 0.000 title claims abstract description 54
- 238000004519 manufacturing process Methods 0.000 title claims description 13
- 239000003245 coal Substances 0.000 claims abstract description 10
- 239000002245 particle Substances 0.000 claims abstract description 6
- 239000002994 raw material Substances 0.000 abstract description 6
- 238000000034 method Methods 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- 238000010791 quenching Methods 0.000 abstract 1
- 230000000171 quenching effect Effects 0.000 abstract 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 6
- 239000000377 silicon dioxide Substances 0.000 description 3
- 239000004575 stone Substances 0.000 description 3
- 238000004939 coking Methods 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
Landscapes
- Coke Industry (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】この発明は、焼結鉱用コークスを
製造するコークスを製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing coke for use in sintered ore.
【0002】0002
【従来の技術】焼結鉱を製造するときには、燃料として
コークスを使用する。この焼結鉱製造用コークスとして
使用されるコークスは、従来次のようなものが使用され
ていた。
(1)高炉用コークス生産時に発生する粉コークス(2
)高炉用コークスを粉砕したコークス(3)コークス乾
式消火装置で発生する微粉コークスBACKGROUND OF THE INVENTION When producing sintered ore, coke is used as a fuel. Conventionally, the following types of coke have been used as coke for producing sintered ore. (1) Coke powder generated during blast furnace coke production (2)
) Coke made by crushing coke for blast furnaces (3) Fine coke generated in coke dry extinguishing equipment
【0003】0003
【発明が解決しようとする課題】しかしながら、従来の
焼結鉱製造用コークスとして使用されるコークスには次
のような問題点があった。
(1)供給可能コークス量が高炉用コークス生産量に左
右される。
(2)原料である石炭の価格が高い。
(3)焼結鉱の歩留が低い。
(4)灰分が低いので、焼結鉱製造時に強度を維持する
ための珪石を配合する必要がある。
(5)コークスを粉砕する費用がかかる。
(6)コークス搬送時に発塵する。[Problems to be Solved by the Invention] However, the coke used as conventional coke for producing sintered ore has the following problems. (1) The amount of coke that can be supplied depends on the production amount of blast furnace coke. (2) The price of coal, which is a raw material, is high. (3) The yield of sintered ore is low. (4) Since the ash content is low, it is necessary to mix silica stone to maintain strength during the production of sintered ore. (5) Crushing coke is expensive. (6) Dust is generated during coke transportation.
【0004】この発明は、上述した従来の焼結鉱製造用
コークスの問題点を解消し、かつ副産物のガスやタール
の生産量が多くなるコークス製造方法を提供することを
目的としている。An object of the present invention is to provide a method for producing coke which solves the above-mentioned problems of the conventional coke for producing sintered ore and which increases the amount of gas and tar produced as by-products.
【0005】[0005]
【課題を解決するための手段】この発明に係るコークス
製造方法は、灰分が9%以上14%以下、揮発分が33
%以上37%以下配合炭を使用し、コークス乾式消火装
置出口でのコークス強度(DI3015)が80以上9
0以下、並びにコークス粒度が35mm以上48mm以
下となるように操業するものである。[Means for Solving the Problems] The coke manufacturing method according to the present invention has an ash content of 9% to 14% and a volatile content of 33%.
% or more and 37% or less blended coal is used, and the coke strength (DI3015) at the outlet of the coke dry extinguishing system is 80 or more and 9
0 or less, and the coke particle size is 35 mm or more and 48 mm or less.
【0006】[0006]
【作用】この発明に係るコークス製造方法は、灰分が9
%以上14%以下、揮発分が33%以上37%以下配合
炭を使用し、コークス乾式消火装置出口でのコークス強
度(DI3015)が80以上90以下、並びにコーク
ス粒度が35mm以上48mm以下となるように操業す
る。
その理由は次のとおりである。[Operation] The coke manufacturing method according to the present invention has an ash content of 9
% or more and 14% or less, volatile content is 33% or more and 37% or less, and the coke strength (DI3015) at the outlet of the coke dry extinguishing system is 80 or more and 90 or less, and the coke particle size is 35 mm or more and 48 mm or less. The company will operate in The reason is as follows.
【0007】(1)配合炭の灰分
9%以上としたのは、これ未満ではコークス強度が低い
からであり、14%以下としたのは、これを超えると原
料コストが高くなり、珪石低減効果が相殺されるからで
ある。(1) The ash content of the blended coal is set to 9% or more because coke strength is low if it is less than this, and the reason why the ash content is set to 14% or less is that if it exceeds this, the raw material cost increases and the silica stone reduction effect is reduced. This is because they cancel each other out.
【0008】(2)配合炭の揮発分
33%以上としたのは、これ未満ではコークス強度が低
いからであり、37%以下としたのは、これを超えると
ガス、タールの発生量が減少するからである。(2) The reason why the volatile content of the blended coal is set to 33% or more is because coke strength is low if it is less than this, and the reason why it is set to 37% or less is because if it exceeds this, the amount of gas and tar generated decreases. Because it does.
【0009】(3)コークス強度
80以上としたのは、これ未満では粉砕コストが上昇し
、原料コストが上昇するからであり、90としたのは、
これを超えると窯出しが困難になるからである。(3) The reason why the coke strength is set at 80 or more is because if it is less than this, the crushing cost increases and the raw material cost increases.The reason why the coke strength is set at 90 is because
This is because if it exceeds this, it becomes difficult to take it out of the kiln.
【0010】(4)コークス粒度
35mm以上としたのは、これ未満では粉砕コストが上
昇し、原料コストが上昇するからであり、48mm以下
としたのは、これを超えるとコークス乾式消火装置での
消火が困難になるからである。(4) The reason why the coke particle size is set at 35 mm or more is because if it is smaller than this, the crushing cost increases and the raw material cost increases, and the reason why the coke particle size is set at 48 mm or less is that if it exceeds this, it will This is because it becomes difficult to extinguish the fire.
【0011】[0011]
【実施例】本発明の1実施例のコークス製造方法により
製造したコークスを使用して焼結鉱を製造したときの焼
結鉱歩留、製造したコークスの原料炭コスト、粉砕費お
よび強度、このコークスを製造したときに発生するガス
およびタールの歩留を、従来の方法で製造した場合と比
較して表1に示す。なお、焼結鉱歩留、原料炭コストお
よび粉砕費は本製造方法を1として指数的に表示した。[Example] Sintered ore yield when sintered ore is manufactured using coke manufactured by the coke manufacturing method of one example of the present invention, coking coal cost, crushing cost and strength of the manufactured coke, Table 1 shows the yields of gas and tar generated when coke is produced in comparison with those produced by conventional methods. Incidentally, the sintered ore yield, coking coal cost, and pulverization cost were expressed exponentially with this production method as 1.
【0012】0012
【表1】[Table 1]
【0013】表1から明らかなように、コークス強度が
若干下がり、粉砕費が粉コークスに対してやや高くなる
ものの、その他の項目においては、従来の方法の場合よ
りよい操業成績を上げている。[0013] As is clear from Table 1, although the coke strength is slightly lower and the crushing cost is slightly higher than coke breeze, in other respects the operating results are better than in the conventional method.
【0014】[0014]
【発明の効果】この発明により、供給可能コークス量が
高炉用コークス生産量に左右されず、原料である石炭の
価格が安くなり、焼結鉱の歩留が高くなり、灰分が高い
ので焼結鉱製造時に強度を維持するための珪石を配合す
る必要がなく、コークスを粉砕する費用が高炉用コーク
スよりも安く、コークス搬送時に発塵しないという効果
がある。[Effects of the invention] With this invention, the amount of coke that can be supplied is not affected by the production volume of coke for blast furnaces, the price of raw material coal is lower, the yield of sintered ore is higher, and the ash content is high, so sintering There is no need to add silica stone to maintain strength during ore production, the cost of crushing coke is lower than coke for blast furnaces, and there are advantages in that no dust is generated during coke transportation.
Claims (1)
33%以上37%以下配合炭を使用し、コークス乾式消
火装置出口でのコークス強度(DI3015)が80以
上90以下、並びにコークス粒度が35mm以上48m
m以下となるように操業することにより焼結鉱用コーク
スを製造することを特徴とするコークス製造方法。Claim 1: Using a blended coal with an ash content of 9% or more and 14% or less and a volatile content of 33% or more and 37% or less, the coke strength (DI3015) at the outlet of the coke dry extinguishing system is 80 or more and 90 or less, and the coke particle size is is 35mm or more 48m
1. A method for producing coke, characterized in that coke for sintered ore is produced by operating the coke so that the coke becomes less than m.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2455891A JPH04264195A (en) | 1991-02-19 | 1991-02-19 | Production of coke |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2455891A JPH04264195A (en) | 1991-02-19 | 1991-02-19 | Production of coke |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04264195A true JPH04264195A (en) | 1992-09-18 |
Family
ID=12141489
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2455891A Pending JPH04264195A (en) | 1991-02-19 | 1991-02-19 | Production of coke |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04264195A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9718963B2 (en) | 2010-04-27 | 2017-08-01 | Aditya Birla Nuvo Limited | Carbon black reactor |
-
1991
- 1991-02-19 JP JP2455891A patent/JPH04264195A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9718963B2 (en) | 2010-04-27 | 2017-08-01 | Aditya Birla Nuvo Limited | Carbon black reactor |
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